Cryogenic production of krypton and xenon from air

Claim 2

In a process for the production of krypton and xenon from a liquid feed stream comprising oxygen, methane, krypton and xenon in a krypton/xenon cryogenic distillation column system having at least one distillation column, wherein the liquid feed stream is introduced to the krypton/xenon cryogenic distillation column system for fractionation into an bottoms liquid enriched in krypton and xenon and an overhead lean in krypton and xenon and said krypton/xenon cryogenic distillation column system has a region wherein oxygen is enriched, the improvement for simultaneously maximizing the concentration of krypton and xenon and the rejection of methane comprises operating said region wherein oxygen is enriched so that ratio of liquid to vapor flow is in the range between 0.05 and 0.2.

Claim 3

The process of claim 1 wherein the ratio of liquid to vapor flow is 0.1.

Claim 4

The process of claim 1 which further comprises removing any C 2 + hydrocarbons and nitrous oxide from the liquid feed stream in an adsorber prior to introducing the feed stream to the krypton/xenon distillation column system.

Claim 5

In a process for the production of krypton and xenon from a liquid feed stream comprising oxygen, methane, krypton and xenon in a single krypton/xenon cryogenic distillation column, wherein the liquid feed stream is introduced to the bottom of the single distillation column for fractionation into an bottoms liquid enriched in krypton and xenon and an overhead lean in krypton and xenon and the single distillation column has a region wherein oxygen is enriched, the improvement for simultaneously maximizing the concentration of krypton and xenon and the rejection of methane comprises operating said region wherein oxygen is enriched so that ratio of liquid to vapor flow is in the range between 0.05 and 0.2.

Claim 6

In a process for the production of krypton and xenon from a liquid feed stream comprising oxygen, methane, krypton and xenon in a single krypton/xenon cryogenic distillation column, wherein the liquid feed stream is introduced to the bottom of the single distillation column for fractionation into an bottoms liquid enriched in krypton and xenon and an overhead lean in krypton and xenon and the single distillation column has a region wherein oxygen is enriched, the improvement for simultaneously maximizing the concentration of krypton and xenon and the rejection of methane comprises operating said region wherein oxygen is enriched so that ratio of liquid to vapor flow is in the range between 0.05 and 0.2.

Claim 7

The process of claim 4 wherein an effective amount of reflux is provided to said oxygen enriching region of the krypton/xenon distillation column system by introducing at least a portion of the liquid feed stream to the top of said region so as to allow operation of said region within the liquid to vapor flow range.

Claim 8

The process of claim 4 wherein an effective amount of reflux is provided to said oxygen enriching region of the krypton/xenon distillation column system by condensing at least a portion of the overhead and returning said condensed portion to the top of said region so as to allow operation of said region within the liquid to vapor flow range.

Claim 9

The process of claim 4 wherein an effective amount of reflux is provided to said oxygen enriching region of the krypton/xenon distillation column system by introducing an oxygen containing liquid stream removed from an appropriate location of a low pressure column of an air separation unit to the top of said region so as to allow operation of said region within the liquid to vapor flow range; and which further comprises removing liquid descending the single distillation column at a location above the bottom liquid feed to the single distillation column; combining said removed liquid into the liquid feed stream, and then removing any C 2 + hydrocarbons and nitrous oxide from the liquid feed stream in an adsorber prior to introducing the feed stream to the single distillation column.

Claim 10

The process of claim 4 wherein an effective amount of reflux is provided to said oxygen enriching region of the krypton/xenon distillation column system by introducing an oxygen containing liquid stream removed from an appropriate location of a low pressure column of an air separation unit to the top of said region in combination with an effective amount of additional reflux is provided by introducing at least a portion of the liquid feed stream to an intermediate location of said region so as to allow operation of said region within the liquid to vapor flow range; and which further comprises removing liquid descending the single distillation column at a location above point of introduction of the additional reflux; combining said removed liquid into the liquid feed stream; then removing any C 2 + hydrocarbons and nitrous oxide from the liquid feed stream in an adsorber prior to removing a portion of the liquid feed for the additional reflux and introducing the remaining portion to the single distillation column.

Claim 11

In a process for the production of krypton and xenon from a liquid feed stream comprising oxygen, methane, krypton and xenon in a krypton/xenon cryogenic distillation system comprising a first and a second distillation column, wherein a first portion of the liquid feed stream is introduced into the top of the first distillation column for fractionation into a first bottoms liquid and a first overhead, wherein a second portion of the liquid feed stream is introduced into the top of the second distillation column for fractionation into a second bottoms and a second overhead, wherein a vapor stream is withdrawn from an intermediate location of the first distillation column and fed to the bottom of the second distillation column and wherein the second bottoms liquid is withdrawn and fed to the intermediate location of the first distillation column, the improvement for simultaneously maximizing the concentration of krypton and xenon and the rejection of methane comprises operating said second distillation column so that ratio of liquid to vapor flow is in the range between 0.05 and 0.2.

Claim 12

In a process for the production of krypton and xenon from a liquid feed stream comprising oxygen, methane, krypton and xenon in a krypton/xenon cryogenic distillation system comprising a first and a second distillation column, wherein a first portion of the liquid feed stream is introduced into the top of the first distillation column for fractionation into a first bottoms liquid and a first overhead, wherein a second portion of the liquid feed stream is introduced into the top of the second distillation column for fractionation into a second bottoms and a second overhead, wherein a vapor stream is withdrawn from an intermediate location of the first distillation column and fed to the bottom of the second distillation column and wherein the second bottoms liquid is withdrawn and fed to the intermediate location of the first distillation column, the improvement for simultaneously maximizing the concentration of krypton and xenon and the rejection of methane comprises operating said second distillation column so that ratio of liquid to vapor flow is in the range between 0.05 and 0.2.

Claim 13

The process of claim 9 which further comprises removing any C 2 + hydrocarbons and nitrous oxide from the first and second portions o the liquid feed stream in an adsorber prior to introducing the feed stream to the krypton/xenon distillation column system.

Claim 14

In a process for the production of krypton and xenon from a liquid feed stream comprising oxygen, methane, krypton and xenon in a krypton/xenon cryogenic distillation system comprising a first and a second distillation column, wherein the liquid feed stream is introduced into the top of the first distillation column for fractionation into a first bottoms liquid and a first overhead, wherein a vapor stream is withdrawn from an intermediate location of the first distillation column and fed to the bottom of the second distillation column for rectification, wherein the second bottoms liquid is withdrawn and fed to the intermediate location of the first distillation column and wherein reflux is provided to the second distillation column by condensing at least a portion of the second column overhead and returning said condensed overhead portion to the top of the second distillation column, the improvement for simultaneously maximizing the concentration of krypton and xenon and the rejection of methane comprises operating said second distillation column so that ratio of liquid to vapor flow is in the range between 0.05 and 0.2.

Claim 15

In a process for the production of krypton and xenon from a liquid feed stream comprising oxygen, methane, krypton and xenon in a krypton/xenon cryogenic distillation system comprising a first and a second distillation column, wherein the liquid feed stream is introduced into the top of the first distillation column for fractionation into a first bottoms liquid and a first overhead, wherein a vapor stream is withdrawn from an intermediate location of the first distillation column and fed to the bottom of the second distillation column for rectification, wherein the second bottoms liquid is withdrawn and fed to the intermediate location of the first distillation column and wherein reflux is provided to the second distillation column by condensing at least a portion of the second column overhead and returning said condensed overhead portion to the top of the second distillation column, the improvement for simultaneously maximizing the concentration of krypton and xenon and the rejection of methane comprises operating said second distillation column so that ratio of liquid to vapor flow is in the range between 0.05 and 0.2.

Claim 16

The process of claim 10 which further comprises removing any C 2 + hydrocarbons and nitrous oxide from the liquid feed stream in an adsorber prior to introducing the feed stream to the krypton/xenon distillation column system.